US6353138B1ExpiredUtility

Process for purifying aqueous tertiary amine and alkanolamine solutions

Priority: May 19, 1999Filed: Apr 18, 2000Granted: Mar 5, 2002
Est. expiryMay 19, 2019(expired)· nominal 20-yr term from priority
Inventors:Peter C. Rooney
C07C 213/10
81
PatentIndex Score
13
Cited by
8
References
11
Claims

Abstract

A process for the removal of primary and secondary amine and alkanolamine impurities from aqueous tertiary amine and alkanolamine solutions without affecting the tertiary amine and/or alkanolamine by treating these solutions with a monoaldehyde or dialdehyde has been described.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
       1. A process for removing primary and secondary amine and alkanolamine impurities from an aqueous tertiary amine or alkanolamine solution used for removal of acid gases from a fluid stream which process comprises treating the aqueous amine or alkanolamine solution with a monoaldehyde in an amount of from about 0.01 to about 1.0 equivalent of the monoaldehyde per one equivalent of the amine or alkanolamine. 
     
     
       2. The process according to  claim 1  wherein the monoaldehyde is formaldehyde. 
     
     
       3. The process according to any one of  claims 1  to  2  wherein the monoaldehyde is added to a circulating amine or alkanolamine plant solution over a period of about 1 to 22 hours. 
     
     
       4. The process according to any one of  claims 1  to  2  wherein the amine or alkanolamine solution is treated with the monoaldehyde in a vessel and then reclaimed by distillation or vacuum distillation. 
     
     
       5. The process according to  claim 1  or  claim 2  wherein the monoaldehyde and hydrogen are added to the circulating amine or alkanolamine plant solution. 
     
     
       6. A process for removing primary and secondary amine and alkanolamine impurities from an aqueous tertiary amine or alkanolamine solution used for removal of acid gases from a fluid stream which process comprises treating the aqueous amine or alkanolamine solution with less than one equivalent of a dialdehyde per equivalent of the amine or alkanolamine. 
     
     
       7. The process according to  claim 6  wherein the dialdehyde is used in an amount of about 0.01 to about 0.99 equivalent of a dialdehyde per equivalent of the amine or alkanolamine in the solution treated. 
     
     
       8. The process according to  claim 6  wherein the dialdehyde is glyoxal. 
     
     
       9. The process according to any one of  claims 6  to  8  wherein the dialdehyde is added to a circulating amine or alkanolamine plant solution over a period of about 1 to 22 hours. 
     
     
       10. The process according to any one of  claims 6  to  8  wherein the amine or alkanolamine solution is treated with the dialdehyde in a vessel and then reclaimed by distillation or vacuum distillation. 
     
     
       11. The process according to any one of  claims 6  to  8  wherein the dialdehyde and hydrogen are added to the circulating amine or alkanolamine plant solution.

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